Asphalt-based reactive hot melt polyurethane adhesive

ABSTRACT

A novel hot melt adhesive that includes a blend of hot melt polyurethane and petroleum liquid.

The present invention is a divisional of U.S. patent application Ser. No. 12/470,912 filed May 13, 2009, which claims priority on U.S. Provisional Patent Application Ser. No. 61/057,961 filed Jun. 2, 2008, which is incorporated herein by reference.

The present invention is directed to the production of a reactive polyurethane hot melt that is blended with asphalt, bitumen, modified bitumen, and/or coal-tar, which then can be used as an interply adhesive.

BACKGROUND OF THE INVENTION

Despite their waterproofing properties, regular “hot mopped” roofing asphalts used by roofing contractors are typically brittle and cool very quickly. If the contractor does not unroll a roof membrane and apply the roof membrane to the hot asphalt within about 2-5 seconds after applying the hot asphalt to the roof surface, the asphalt will cool and thus will not properly adhere to the underside of the membrane when the membrane is place over the cooled asphalt. Areas of the underside of the membrane that do not properly adhere to the asphalt are prone to delaminating and/or blistering over time.

In view of the deficiencies associated with the use of hot mopped asphalt as an interply adhesive for roof membranes, there is a need for a improved or modified material that can be used to overcome the past problems with the use of “hot mopped” asphalt.

SUMMARY OF THE INVENTION

The present invention is directed to roof membrane adhesion products, more particularly to hot melt asphalt, modified asphalt, bitumen, modified bitumen, coal-tar, and/or modified coal tar products that are used to adhere roof membrane plies to one another and/or to a roof deck of a building or other type of structure, and even more particularly to hot melt asphalt, modified asphalt, bitumen, modified bitumen, coal-tar, and/or modified coal tar products that are blended with a polyurethane material to form a reactive polyurethane hot melt material that can be used to adhere roof membrane plies to one another and/or to a roof deck of a building or other type of structure.

Because asphalt, modified asphalt, bitumen, modified bitumen, coal-tar, and/or modified coal tar products have the ability to take on the properties of the rubber blended into it, an asphalt-based reactive hot melt polyurethane adhesive blend, a modified asphalt-based reactive hot melt polyurethane adhesive blend, a bitumen-based reactive hot melt polyurethane adhesive blend, a modified bitumen-based reactive hot melt polyurethane adhesive blend, a coal tar-based reactive hot melt polyurethane adhesive blend, and/or a modified coal tar-based reactive hot melt polyurethane adhesive blend can be formed that has water repellant properties of asphalt, modified asphalt, bitumen, modified bitumen, coal-tar, and/or modified coal tar while having additional bonding strength that can be at least partially associated with the polyurethane. Such a novel blend can be tailor-made so as to increase the time period an installer can lay a roof membrane on the blend and still create a strong bond between the roof surface, the blend and the roof membrane. As such, an installer would not have to hurry and apply a ply of roof membrane (e.g., modified bitumen membrane, etc.) on the roof after the hot-melt blend of the present invention is applied to the surface of the roof.

In addition to or alternative to extending the time period for applying a roof membrane on the blend, the blend of the present invention can be formulated to enhance the adhesive properties of the blend by including tackifying resins and/or other additives in the blend to impart a tape-like tack that can act as a mechanical bond, thereby holding a roof membrane to the blend and/or roof surface during the polyurethane curing process.

The blend of the present invention can be used in the following non-limiting applications, namely:

A. A high strength interply adhesive for a built-up roof system as an alternative to the standard “hot mop” method.

B. An inline adhesive for the application of single ply membranes (i.e., white membranes, solar panels, etc.) on asphalt, modified asphalt, bitumen, modified bitumen, coal-tar, and/or modified coal tar roofing during manufacturing.

In one non-limiting aspect of the present invention, a hot melt polyurethane is combined with asphalt, modified asphalt, bitumen, modified bitumen, coal-tar, and/or modified coal tar to form the blend of the present invention. For purposes of this invention, term “petroleum liquid” will be hereinafter used to generically refer to all types of asphalt, modified asphalt, bitumen, modified bitumen, coal-tar, modified coal tar, or any mixture thereof, unless a specific type of type of asphalt, modified asphalt, bitumen, modified bitumen, coal-tar, or modified coal tar is referenced. In one non-limiting embodiment of the invention, the hot melt polyurethane is a one-component, moisture-curing polyurethane based on acrylate and/or methacrylate polymers or copolymers. In one non-limiting formulation of the invention, the moisture-curing polyurethane includes at least one reaction product with reactive isocyanate groups that are obtained by reaction of at least one di- or polyisocyanate with one or more polyether-polyols, partly crystalline or crystalline polyester-polyols and/or low molecular weight polymers from olefinically unsaturated monomers, and/or optionally tackifying resins. The monomeric di- or polyisocyanates suitable for the preparation of the hot melt polyurethane generally are those aromatic, aliphatic or cycloaliphatic diisocyanates having molecular weights of up to about 500; however, higher molecular weights can be used. Non-limiting examples of suitable aromatic diisocyanates include isomers of toluylene diisocyanate (TDI), naphthalene 1,5-diisocyanate (NDI), naphthalene 1,4-diisocyanate (NDI), diphenylmethane 4,4′-diisocyanate (MDI), diphenylmethane 2,4′-diisocyanate and mixtures of 4,4′-diphenylmethane diisocyanate with the 2,4′ isomer, xylylene diisocyanate (XDI), 4,4′-diphenyl-dimethylmethane diisocyanate, di- and tetraalkyl-diphenylmethane diisocyanates, 4,4′-dibenzyl diisocyanate, 1,3-phenylene diisocyanate and 1,4-phenylene diisocyanate. Non-limiting examples of cycloaliphatic diisocyanates include 4,4′-dicyclohexylmethane diisocyanate (H₁₂MDI), 1-isocyanatomethyl-3-isocyanato-1,5,5-trimethyl-cyclohexane (isophorone diisocyanate, IPDI), cyclohexane 1,4-diisocyanate, hydrogenated xylylene diisocyanate (H₆XDI), 1-methyl-2,4-diisocyanato-cyclohexane, m- or p-tetramethylxylene diisocyanate (m-TMXDI, pTMXDI) and dimer fatty acid diisocyanate. Non-limiting examples of aliphatic diisocyanates are tetramethoxybutane 1,4-diisocyanate, butane 1,4-diisocyanate, hexane 1,6-diisocyanate (HDI), 1,6-diisocyanato-2,2,4-trimethylhexane, 1,6-diisocyanato-2,4,4-trimethylhexane, lysine diisocyanate and 1,12-dodecane diisocyanate (C₁₂DI).y used. Non-limiting examples of polypropylene glycols or polybutylene glycols which can be used include di- and/or trifunctional polypropylene glycols with two or more hydroxyl groups per molecule in the molecular weight range from 400-20,000. Random and/or block copolymers of ethylene oxide and propylene oxide can also be employed. Another group of polyethers which can be used are polytetramethylene glycols (polybutylene glycols, poly(oxytetramethylene) glycol, poly-THF), wherein the molecular weight range of the polytetramethylene glycols are from 600-6,000. Instead of or additional to polyether-polyols, low molecular weight polyols, alkylene diols (e.g., butanediol, hexanediol, octanediol, decanediol, dodecanediol, etc.) can also be used. Non-limiting examples of polyester-polyols that can be used are the crystalline or partly crystalline polyester-polyols which can be prepared by condensation of di- or tricarboxylic acids (e.g., adipic acid, sebacic acid, glutaric acid, azelaic acid, suberic acid, undecanedioic acid, dodecandioic acid, 3,3-dimethylglutaric acid, terephthalic acid, isophthalic acid, hexahydrophthalic acid, etc.), dimer fatty acid with low molecular weight diols or triols (e.g., ethylene glycol, propylene glycol, diethylene glycol, triethylene glycol, dipropylene glycol, 1,4-butanediol, 1,6-hexanediol, 1,8-octanediol, 1,10-decanediol, 1,12-dodecanediol, dimer fatty alcohol, glycerol, trimethylolpropane, etc.). One non-limiting specific example of a hot melt polyurethane that can be used in the blend of the present invention includes at least about 2 weight percent of a diisocyanate, at least about 10 weight percent of a difunctional polypropylene glycol with a molecular weight of from about 1,000-8,000, at least about 0.5 weight percent of a polypropylene glycol or alkylene diol with a molecular weight from about 100-900, at least about 5 weight percent of a crystalline or partly crystalline polyester-polyol, at least about 2 weight percent of a low molecular weight polymer of olefinically unsaturated monomers, at least about 0.1 weight percent of a hydroxylated tackifying resin, and at least 0.005 weight percent of an acid stabilizer. Another non-limiting specific example of a hot melt polyurethane that can be used in the blend of the present invention includes at least 5 weight percent of a diisocyanate, at least about 15 weight percent of a difunctional polypropylene glycol with a molecular weight of from about 1,500-7,000, at least about 1 weight percent of a polypropylene glycol or alkylene diol with a molecular weight from about 150-800, at least about 10 weight percent of a crystalline or partly crystalline polyester-polyol, at least about 5 weight percent of a low molecular weight polymer of olefinically unsaturated monomers, at least about 1 weight percent of a hydroxylated tackifying resin, and at least about 0.01 weight percent of an acid stabilizer. Still another non-limiting specific example of a hot melt polyurethane that can be used in the blend of the present invention includes about 5-15 weight percent of a diisocyanate, about 20-40 weight percent of a difunctional polypropylene glycol with a molecular weight of from about 2,000-6,000, about 2-8 weight percent of a polypropylene glycol or alkylene diol with a molecular weight from about 200-600, about 15-30 weight percent of a crystalline or partly crystalline polyester-polyol, about 10-35 weight percent of a low molecular weight polymer of olefinically unsaturated monomers, about 2-8 weight percent of a hydroxylated tackifying resin, and about 0.01-0.1 weight percent of an acid stabilizer. Yet non-limiting specific example of a hot melt polyurethane that can be used in the blend of the present invention includes at least one reaction product with reactive NCO groups produced by reaction of i) about 5-15 weight percent of at least one di- or polyisocyanate; ii) about 20-40 weight percent difunctional polypropylene glycol having a molecular weight of from about 2,000 to 6,000; iii) about 15-30 weight percent of at least one crystalline or partly crystalline polyester-polyol; iv) about 10-35 weight percent of at least one low molecular weight polymer obtained by polymerization of one or more olefinically unsaturated monomers; v) about 2-8 weight percent of a polypropylene glycol or alkylene diol having a molecular weight of from about 200 to 600; and iv) about 2-8 weight percent of a tackifying resin. Still yet another non-limiting specific example of a hot melt polyurethane that can be used in the blend of the present invention includes i) a reactive, moisture-curable polyurethane adhesive; and ii) a catalytically effective amount comprising at least about 0.005 weight percent of at least one tertiary amine non-fugitive catalyst containing at least one active hydrogen, that provides at least one functional group that is capable of reacting with one or more isocyanate groups in a polyurethane prepolymer. In one non-limiting formulation of this embodiment, the hot melt polyurethane includes polyols. Still yet another non-limiting specific example of a hot melt polyurethane that can be used in the blend of the present invention is disclosed in U.S. Pat. Nos. 6,465,104; 6,635,722 and 7,300,996, all of which are incorporated herein.

In another and/or alternative non-limiting aspect of the present invention, the petroleum liquid that can be used in the blend of the present invention can have a wide range of softening points and penetrations. In one embodiment of the invention, the petroleum liquid has a penetration value of 2-30 and a softening point of about 130° F.-190° F. In another non-limiting embodiment of the invention, the petroleum liquid has a penetration value of 2-25 and a softening point of about 150° F.-180° F. In still another non-limiting embodiment of the invention, the petroleum liquid has a penetration value of 2-20 and a softening point of about 150° F.-170° F. In yet another non-limiting embodiment of the invention, the petroleum liquid has a penetration value of 12-20 and a softening point of about 155° F.-165° F.

In still another and/or alternative non-limiting aspect of the present invention, the blend of petroleum liquid with hot melt polyurethane can be used to form an interply adhesive for roofing materials and roofing systems. In one non-limiting embodiment, a reactive hot melt polyurethane can created using a variety of different polyol and diisocyanate combinations along with one or more additives, and that such reactive hot melt polyurethane can be tailor-made to produce very strong roofing products. The reactive hot melt polyurethane additives can be selected to impart one or more desirable properties to the blend of petroleum liquid with hot melt polyurethane such as tape-like tackiness, which would act as a mechanical clamp to hold the roof membranes together while the petroleum liquid-based polyurethane cured over time.

In still yet another and/or alternative non-limiting aspect of the present invention, the blend of petroleum liquid with hot melt polyurethane can be used in an inline manufacturing process to form roofing materials. In such a manufacturing process, the blend of the present invention can be applied to a roof membrane (i.e., white reflective membrane, solar panel, modified bitumen, etc.) and then mated with another roof membrane during the same manufacturing process to form a laminated roof membrane that could be shipped out to a customer.

Non-limiting examples of the invention are set forth below:

EXAMPLE 1

Diisocyanate and/or polyisocynate 5-50 wt % Petroleum liquid 5-80 wt % Polyester-polyol, polypropylene glycol, 5-90 wt % polybutylene glycol, olefinically unsaturated monomers, and/or alkylene diols

EXAMPLE 2

Diisocyanate and/or polyisocynate 10-45 wt % Petroleum Liquid  5-70 wt % Polyester-polyol, polypropylene glycol, 10-85 wt % polybutylene glycol, olefinically unsaturated monomers, and/or alkylene diols

EXAMPLE 3

Acid stabilizer up to 2 wt % Diisocyanate and/or polyisocynate 10-40 wt % Petroleum Liquid 5-65 wt % Catalyst up to 5 wt % Polyester-polyol, polypropylene glycol, 15-85 wt % polybutylene glycol, olefinically unsaturated monomers, and/or alkylene diols Tackifying resin up to 15 wt %

EXAMPLE 4

Acid stabilizer up to 1 wt % Aromatic diisocyanate 10-35 wt % and/or aromatic polyisocynate Petroleum Liquid 5-65 wt % Catalyst up to 3 wt % Polyester-polyol, polypropylene glycol, 10-85 wt % polybutylene glycol, olefinically unsaturated monomers, and/or alkylene diols Tackifying resin up to 10 wt %

EXAMPLE 5

Acid stabilizer up to 1 wt % Catalyst up to 3 wt % Propylene Glycol (500-3000 MW) 15-80 wt. % Polyester Polyol 10-30 wt. % MDI 15-30 wt % Type I-III Asphalt 5-60 wt. % Tackifying resin up to 10 wt %

EXAMPLE 6

Acid stabilizer up to 0.8 wt % Catalyst up to 2 wt % Propylene Glycol (800-1200 MW) 20-30 wt. % Propylene Glycol (1800-2400 MW) 20-30 wt. % Polyester Polyol 15-25 wt. % MDI 10-20 wt % Type I-III Asphalt 5-35 wt. % Tackifying resin up to 8 wt %

EXAMPLE 7

Acid stabilizer 0.005-0.5 wt % Catalyst 0.005-1.5 wt % Propylene Glycol (800-1200 MW) 22-27 wt. % Propylene Glycol (1800-2400 MW) 22-27 wt. % Polyester Polyol 20-23 wt. % MDI 15-18 wt % Type III Asphalt 5-21 wt. % Tackifying resin 0.1-8 wt %

EXAMPLE 8

Acid stabilizer 0.01-0.4 wt % Catalyst 0.005-1 wt % Propylene Glycol (800-1200 MW) 10-25 wt. % Propylene Glycol (1800-2400 MW) 10-25 wt. % Polyester Polyol 10-20 wt. % Acrylic Copolymer 10-25 wt. % MDI 10-20 wt % Type I-III Asphalt 5-50 wt. % Tackifying resin 0.1-6 wt %

EXAMPLE 9

Acid stabilizer 0.01-0.2 wt % Catalyst 0.005-0.5 wt % Propylene Glycol (800-1200 MW) 15-20 wt. % Propylene Glycol (1800-2400 MW) 15-20 wt. % Polyester Polyol 12-27 wt. % Acrylic Copolymer 15-20 wt. % MDI 15-18 wt % Type III Asphalt 5-28 wt. % Tackifying resin 0.2-6 wt %

EXAMPLE 10

Acid stabilizer up to 5 wt % Catalyst up to 10 wt % Diisocyanate and/or polyisocynate at least 5 wt % Petroleum Liquid at least 5 wt % Polyester-polyol, polypropylene glycol, at least 5 wt % polybutylene glycol, olefinically unsaturated monomers, and/or alkylene diols Acrylic Copolymer up to 30 wt. % Tackifying resin up to 20 wt %

EXAMPLE 11

Acid stabilizer up to 4 wt % Catalyst up to 6 wt % Diisocyanate and/or polyisocynate 5-50 wt % Petroleum Liquid 5-80 wt % Polyester-polyol, polypropylene glycol, 5-90 wt % polybutylene glycol, olefinically unsaturated monomers, and/or alkylene diols Acrylic Copolymer up to 25 wt. % Tackifying resin up to 15 wt %

In the examples above, Examples 1 and 2 illustrate the reactive polyurethane hot melt of the present invention includes three principal components, namely 1) diisocyanate and/or polyisocynate, 2) petroleum liquid, and 3) polyester-polyol, polypropylene glycol, polybutylene glycol, olefinically unsaturated monomers, and/or alkylene diols. As illustrated in Examples 3-9, the reactive polyurethane hot melt of the present invention generally also includes one or more of the following components, namely a) acid stabilizer, b) catalyst, and/or c) tackifying resin. As illustrated in Examples 5-9, the third principal component of the reactive polyurethane hot melt of the present invention is generally formed of two or more different compounds, namely two or more compounds selected from the group of polyester-polyol, polypropylene glycol, polybutylene glycol, olefinically unsaturated monomers, and/or alkylene diols. As illustrated in Examples 8 and 9, the reactive polyurethane hot melt of the present invention is generally includes an acrylic copolymer. Examples 10 and 11 illustrated two of the broader aspects of the present invention. As illustrated in Examples 6-9, the weight percent of the second principal component of the reactive polyurethane hot melt of the present invention is generally less than the weight percent of the third principal component of the reactive polyurethane hot melt of the present invention. When the weight percent of the second principal component is less than the weight percent of the third principal component, the weight ratio the second principal component to the third principal component is generally about 0.06-0.98:1, typically about 0.07-0.8:1, more typically about 0.1-0.7:1, and even more typically about 0.2-0.6:1. As also illustrated in Examples 6-9, the weight percent of the first principal component of the reactive polyurethane hot melt of the present invention is generally less than the weight percent of the third principal component of the reactive polyurethane hot melt of the present invention. When the weight percent of the first principal component is less than the weight percent of the third principal component, the weight ratio the first principal component to the third principal component is generally about 0.08-0.9:1, typically about 0.1-0.75:1, more typically about 0.12-0.65:1, and even more typically about 0.15-0.5:1. In one specific composition of reactive polyurethane hot melt of the present invention, the weight percent of the third principal component is greater than the combined weigh percent of the first and second principal components; however, this is not required.

It will thus be seen that the objects set forth above, among those made apparent from the preceding description, are efficiently attained, and since certain changes may be made in the constructions set forth without departing from the spirit and scope of the invention, it is intended that all matter contained in the above description and shown in the accompanying drawings shall be interpreted as illustrative and not in a limiting sense. The invention has been described with reference to preferred and alternate embodiments. Modifications and alterations will become apparent to those skilled in the art upon reading and understanding the detailed discussion of the invention provided herein. This invention is intended to include all such modifications and alterations insofar as they come within the scope of the present invention. It is also to be understood that the following claims are intended to cover all of the generic and specific features of the invention herein described and all statements of the scope of the invention, which, as a matter of language, might be said to fall therebetween. 

1-18. (canceled)
 19. A method of adhering an interply roof membrane to another roof membrane or to a roof deck substrate comprising: a) applying a liquid hot melt adhesive to said roof membrane or said roof deck, said hot-melt adhesive comprising a blend of a) hot melt polyurethane and b) petroleum liquid selected from the group consisting of asphalt, modified asphalt, bitumen, modified bitumen, coal-tar, modified coal tar, or mixtures thereof; and, b) applying said interply roof membrane to said roof membrane or said roof deck, said interply of roof membrane applied to said roof membrane or said roof deck prior to a complete curing of said hot melt polyurethane in said hot melt adhesive.
 20. The method as defined in claim 19, wherein said interply roof membrane is a white reflective membrane, a flexible solar panel, or a modified bitumen roof membrane.
 21. The method as defined in claim 19, wherein said interply roof membrane secured to said roof membrane at a manufacturing site and rolled into a roll of connected membrane.
 22. The method as defined in claim 22, wherein said interply roof membrane and said roof membrane are conveyed through at least one set of pressing rollers, at least one drum roller, or combinations thereof to press said interply roof membrane to said roof membrane prior to the complete curing of said hot melt polyurethane in said hot melt adhesive.
 23. The method as defined in claim 19, wherein said hot melt adhesive comprises: Diisocyanate and/or polyisocynate 5-50 wt % Petroleum Liquid 5-80 wt % Polyester-polyol, polypropylene glycol, 5-90 wt % polybutylene glycol, olefinically unsaturated monomers, and/or alkylene diols.


24. The method as defined in claim 19, including the step of heating said hot melt adhesive to a temperature of greater than 130° F. so as to liquefy said hot melt adhesive prior to applying said hot melt adhesive to said roof membrane or said roof deck.
 25. The method as defined in claim 19, wherein said petroleum liquid has a softening point of at least about 130° F. and a penetration value of about 2-30.
 26. The method as defined in claim 19, wherein said hot melt polyurethane includes a) diisocyanate, polyisocynate, or mixtures thereof, and b) polyester-polyol, polypropylene glycol, polybutylene glycol, olefinically unsaturated monomers, alkylene diols, or mixtures thereof.
 27. The method as defined in claim 26, wherein said hot melt polyurethane includes an acid stabilizer, a catalyst, a tackifying agent, or mixtures thereof.
 28. The method as defined in claim 26, wherein said petroleum liquid has a softening point of at least about 130° F. and a penetration value of about 2-30.
 29. The method as defined in claim 26, wherein a weight percent of said polyester-polyol, polypropylene glycol, polybutylene glycol, olefinically unsaturated monomers, alkylene diols, or mixtures thereof is greater than a weight percent of said diisocyanate, polyisocynate, or mixtures thereof.
 30. The method as defined in claim 29, wherein a weight percent of said polyester-polyol, polypropylene glycol, polybutylene glycol, olefinically unsaturated monomers, alkylene diols, or mixtures thereof is greater than a weight percent of said petroleum liquid.
 31. The method as defined in claim 30, wherein a weight percent of said polyester-polyol, polypropylene glycol, polybutylene glycol, olefinically unsaturated monomers, alkylene diols, or mixtures thereof is greater than a combined weight percent of said petroleum liquid and said diisocyanate, polyisocynate, or mixtures thereof.
 32. The method as defined in claim 19, comprising: Diisocyanate and/or polyisocynate 10-45 wt % Petroleum Liquid  5-70 wt % Polyester-polyol, polypropylene glycol, 10-85 wt % polybutylene glycol, olefinically unsaturated monomers, and/or alkylene diols.


33. The method as defined in claim 19, comprising: Acid stabilizer up to 2 wt % Diisocyanate and/or polyisocynate 10-40 wt % Petroleum Liquid 5-65 wt % Catalyst up to 5 wt % Polyester-polyol, polypropylene glycol, 15-85 wt % polybutylene glycol, olefinically unsaturated monomers, and/or alkylene diols Tackifying resin up to 15 wt %.


34. The method as defined in claim 19, comprising: Acid stabilizer up to 1 wt % Aromatic diisocyanate 10-35 wt % and/or aromatic polyisocynate Petroleum Liquid 5-65 wt % Catalyst up to 3 wt % Polyester-polyol, polypropylene glycol, 10-85 wt % polybutylene glycol, olefinically unsaturated monomers, and/or alkylene diols Tackifying resin up to 10 wt %.


35. The method as defined in claim 19, comprising: Acid stabilizer up to 1 wt % Catalyst up to 3 wt % Propylene Glycol (500-3000 MW) 15-80 wt. % Polyester Polyol 10-30 wt. % MDI 15-30 wt % Type I-III Asphalt 5-60 wt. % Tackifying resin up to 10 wt %.


36. The method as defined in claim 19, comprising: Acid stabilizer up to 0.8 wt % Catalyst up to 2 wt % Propylene Glycol (800-1200 MW) 20-30 wt. % Propylene Glycol (1800-2400 MW) 20-30 wt. % Polyester Polyol 15-25 wt. % MDI 10-20 wt % Type I-III Asphalt 5-35 wt. % Tackifying resin up to 8 wt %.


37. The method as defined in claim 19, comprising: Acid stabilizer 0.005-0.5 wt % Catalyst 0.005-1.5 wt % Propylene Glycol (800-1200 MW) 22-27 wt. % Propylene Glycol (1800-2400 MW) 22-27 wt. % Polyester Polyol 20-23 wt. % MDI 15-18 wt % Type III Asphalt 5-21 wt. % Tackifying resin 0.1-8 wt %.


38. The method as defined in claim 19, comprising: Acid stabilizer 0.01-0.4 wt % Catalyst 0.005-1 wt % Propylene Glycol (800-1200 MW) 10-25 wt. % Propylene Glycol (1800-2400 MW) 10-25 wt. % Polyester Polyol 10-20 wt. % Acrylic Copolymer 10-25 wt. % MDI 10-20 wt % Type I-III Asphalt 5-50 wt. % Tackifying resin 0.1-6 wt %.


39. The method as defined in claim 19, comprising: Acid stabilizer 0.01-0.2 wt % Catalyst 0.005-0.5 wt % Propylene Glycol (800-1200 MW) 15-20 wt. % Propylene Glycol (1800-2400 MW) 15-20 wt. % Polyester Polyol 12-27 wt. % Acrylic Copolymer 15-20 wt. % MDI 15-18 wt % Type III Asphalt 5-28 wt. % Tackifying resin 0.2-6 wt %. 